Natural rubber latex, natural rubber, rubber composition contianing the same, and tire

ABSTRACT

The natural rubber latex of the present invention in which phospholipid contained in the latex is decomposed, particularly the natural rubber latex in which it is decomposed by enzyme treatment with lipase and/or phospholipase at a temperature of 70° C. or lower is excellent in a processability, and in the natural rubber thereof and the rubber composition using the same, the physical properties such as an anti-aging characteristic, a tensile strength and an abrasion resistance are sufficiently maintained. Accordingly, the natural rubber of the present invention can be used as an excellent member for a tire.

TECHNICAL FIELD

The present invention relates to natural rubber latex, natural rubber, a rubber composition thereof and a tire using the same, and it further relates to a production process for such natural rubber.

BACKGROUND ART

In general, natural rubber is frequently used in many fields including industrial products such as tires, rubber belts, rubber rolls, bladders and fenders and sporting goods such as tennis balls, basket balls, soccer balls and volley balls. In a tire, it is used as a material for various components constituting rubber tires, such as treads, side walls, ply coating rubbers and bead fillers.

In recent years, it has become apparent that protein contained in natural rubber is a cause to bring about an allergic symptom, and a lot of deprotenizing techniques have been proposed.

Natural rubber is more excellent in mechanical characteristics than synthetic rubber and has low so-called tan δ (dynamic loss factor). Accordingly, natural rubber is excellent in a low hysteresis loss property, but it is desired to be improved in a gripping property in a wet state. Further, crude natural rubber (rubber used as a raw material) is inferior in processability and a productivity in the production. This is because protein and phospholipid are bonded to a molecular end of natural rubber, so that proteins themselves and phospholipids themselves are further bonded and associated to form a higher order branched structure. In order to solve such problem, a deprotenizing technique in which a total nitrogen content of natural rubber is reduced to 0.1 mass % or less has been proposed (refer to Japanese Patent Application Laid-Open No. 329838/1994). In conventional deprotenizing treatments, natural rubber latex is repeatedly washed with surfactants, and washing thereof is accompanied with centrifugal process. Further, it is carried out to add a proteolytic enzyme to natural rubber latex to decompose protein and then repeatedly wash it with a surfactant, and protease originating in a bacteria is preferably used as the proteolytic enzyme (refer to Japanese Patent Application Laid-Open No. 56902/1994 and Japanese Patent Application Laid-Open No. 56906/1994).

For example, anionic surfactants and/or nonionic surfactants can be used as a surfactant for deprotenizing treatment. The anionic surfactants include, for example, surfactants of a carboxylic acid base, a sulfonic acid base, a sulfate base and a phosphate base.

On the other hand, it is possible to reduce a branch degree of a higher-order branched structure to improve a processability of natural rubber. However, if a deprotenizing technique is used to completely remove protein, a large part of non-rubber components including protein is removed as well, and the satisfactory processability-improving effect can not be obtained. This reduces an aging resistance of a natural rubber. Further, complete deprotenization reduces entanglement of the molecules themselves originating in a polypeptide bond and the apparent molecular weight to a large extent, which results in reducing the tensile force and the abrasion resistance.

DISCLOSURE OF THE INVENTION

An object of the present invention is to provide a natural rubber latex having an excellent processability, natural rubber which is sufficiently maintained in physical properties such as an aging resistance, a tensile force and an abrasion resistance, a production process for the same and a rubber composition and a tire using such natural rubber.

The present inventors decomposed a prescribed bond and an associated part of a branch end, that is, a phospholipid in a higher-order branched structure of natural rubber latex. To be specific, lipase and/or phospholipase enzyme treatment was carried out to try modification of natural rubber such as shortening in stress relaxation time to find that natural rubber was improved in a processability without bringing about a reduction in the physical properties of the natural rubber, and they have come to reach the present invention.

Further, they have found as well that if natural rubber latex is subjected to treatment with protease in combination with such enzyme treatment with lipase and phospholipase, the latex is observed to be further improved in a processability, and they have come to reach the present invention.

That is, the natural rubber latex, the natural rubber and the rubber composition and the tire using the same according to the present invention are characterized by comprising the constitutions and the processes of the following items (1) to (15) and thus solve the problems described above.

-   (1) A natural rubber latex in which phospholipid contained in the     latex is decomposed. -   (2) The natural rubber latex as described in the above item (1),     wherein enzyme treatment with lipase and/or phospholipase is carried     out in the decomposition. -   (3) The natural rubber latex as described in the above item (2),     wherein an addition amount of the lipase and/or the phospholipase     falls in a range of 0.005 to 0.5 mass part per 100 mass parts of the     latex solid component. -   (4) The natural rubber latex as described in the above item (2) or     (3), wherein enzyme treatment with protease is carried out. -   (5) The natural rubber latex as described in any of the above     items (2) to (4), wherein the enzyme treatment is carried out at a     temperature of 70° C. or lower. -   (6) The natural rubber latex as described in any of the above     items (2) to (5), wherein treatment with a surfactant is carried out     in addition to the enzyme treatments. -   (7) A natural rubber obtained from the natural rubber latex as     described in any of the above items (1) to (6). -   (8) The natural rubber as described in the above item (7), wherein a     Mooney viscosity (ML₁₊₄) and a stress relaxation time T₈₀ of the     above rubber satisfy the relation of T₈₀<0.0035exp(ML₁₊₄/8.2)+20 in     a range of 40<ML₁₊₄<100 (provided that ML₁₊₄ is a measured value at     a temperature of 100° C., and T₈₀ is time (second) spent until the     value of ML₁₊₄ is reduced by 80%, that is, reduced to 20% since     rotation of a rotor is stopped immediately after measurement of     ML₁₊₄). -   (9) A rubber composition using the natural rubber as described in     the above item (7) or (8). -   (10) A tire characterized by using the rubber composition as     described in the above item (9). -   (11) A production process for natural rubber, wherein it is produced     by subjecting natural rubber latex to enzyme treatment with lipase     and/or phospholipase. -   (12) The production process for natural rubber as described in the     above item (11), wherein the enzyme treatment is carried out by     adding lipase and/or phospholipase in an amount falling in a range     of 0.005 to 0.5 mass part per 100 mass parts of the latex solid     component. -   (13) The production process for natural rubber as described in the     above item (11) or (12), wherein enzyme treatment with protease is     carried out in addition to the enzyme treatment described above. -   (14) The production process for natural rubber as described in any     of the above items (11) to (13), wherein the enzyme treatment above     is carried out at a temperature of 70° C. or lower. -   (15) The production process for natural rubber as described in any     of the above items (11) to (14), wherein treatment with a surfactant     is carried out in addition to the enzyme treatment.

As described above, in the present invention, phospholipid is partially or selectively decomposed at a branched part of natural rubber latex, and the non-rubber component can be allowed to remain. One of mechanisms for improving the processability includes shortening in stress relaxation time of natural rubber. Selective phospholipid decomposition of natural rubber latex in the present invention shortens stress relaxation time of natural rubber. Accordingly, the natural rubber and the rubber composition using the same are improved in a processability thereof (a shrinking property and a dimensional stability) and can sufficiently maintain an anti-aging property, a tensile strength and an abrasion resistance. The stress relaxation time referred to herein is substituted with T₈₀ in contrast with ML₁₊₄ of Mooney viscosity measurement, and this value has to satisfy the range described in the item (8).

BEST MODE FOR CARRYING OUT THE INVENTION

The natural rubber latex, the natural rubber, the rubber composition, the tire using the same and the production process for natural rubber according to the present invention shall be described below in details. However, the present invention shall not be restricted to the following embodiments.

In the natural rubber latex according to the present invention, phospholipid contained in the latex is decomposed. Natural rubber latex used as the raw material means field latex obtained from natural rubber tree, and either of an ammonia-treated latex which is commercially available and a fresh field latex can be used for the latex.

Usually, protein and phospholipid are bonded to a molecular end of such natural rubber, and it is estimated that proteins themselves and phospholipids themselves at the end thereof are further bonded and associated to form a higher-order branched structure. It is estimated, however, that in natural rubber latex in which phospholipid is decomposed, the phospholipid is decomposed in a branch point of such higher-order branched structure, whereby the branch degree is reduced. If the branch degree is reduced, processability of natural rubber is sufficiently improved. If the higher-order branched structure is completely decomposed, that is, protein is completely removed, a large part of non-rubber components including protein is removed, and the aging resistance and the abrasion resistance are reduced. In contrast with this, a rubber obtained by using natural rubber latex in which phospholipid forming the branch described above is convergently decomposed is not observed to be reduced in anti-aging property and abrasion resistance to a large extent.

Natural rubber latex which is subjected to enzyme treatment with lipase and/or phospholipase can be given as the natural rubber latex in which phospholipid is decomposed according to the present invention.

The lipase and/or phospholipase described above shall not specifically be restricted, and any of those originating in bacteria, hyphomycetes and yeast can be used. Enzyme activity of Lipase and phospholipase is 100 (U/g) or more, preferably 1000 (U/g) or more, more preferably 10000 (U/g) or more and further preferably 100000 (U/g) or more. Lipase M “Amano” 10 (product manufactured by Amano Enzyme Co., Ltd.), Lipase OF (product manufactured by Meito Co., Ltd.) and Phospholipase Al (product manufactured by Sankyo Co., Ltd.) which are commercial products can be given as such lipase and phospholipase.

An addition amount of the lipase and phospholipase described above in such enzyme treatment falls in a range of preferably 0.005 to 0.5 mass part, particularly preferably 0.01 to 0.2 mass part per 100 mass parts of the solid component contained in the natural rubber latex. If the addition amount falls in the range described above, phospholipid contained in the natural rubber latex is suitably decomposed, and the processability and the good physical properties which are the objects are maintained.

If an addition amount (total amount) of the lipase and/or the phospholipase described above is less than 0.005 mass part, the decomposition reaction of phospholipid is unsatisfactory, and the improving effect of the processability is not sufficiently obtained. If an addition amount (total amount) of the lipase and/or the phospholipase described above exceeds 0.5 mass part, almost all of fatty acids contained in the natural rubber is decomposed, and the strain induced crystallinity is reduced, so that the tensile strength and the abrasion resistance are reduced.

The natural rubber latex according to the present invention may further be subjected to enzyme treatment with protease in addition to lipase and/or phospholipase.

The protease described above shall not specifically be restricted as is the case with lipase and phospholipase, and any of those originating in bacteria, hyphomycetes and yeast can be used. Enzyme activity of protease is 100 (U/g) or more, preferably 1000 (U/g) or more, more preferably 10000 (U/g) or more and further preferably 100000 (U/g) or more. Alkalase 2.5L-type DX (manufactured by Novozymes Co., Ltd.) and Proleather FG-F (manufactured by Amano Enzyme Co., Ltd.) which are commercial products can be given as such protease.

An addition amount of the protease in such enzyme treatment falls in a range of preferably 0.005 to 0.5 mass part, particularly preferably 0.01 to 0.2 mass part per 100 mass parts of the solid component contained in the natural rubber latex.

If the addition amount falls in the range described above, protein contained in the natural rubber latex is suitably decomposed, and the processability which is the object is further improved. Further, the good physical properties are maintained. If an addition amount of the protease is less than the range described above, the decomposition reaction of the protein is unsatisfactory, and therefore it is not preferred. On the other hand, if the addition amount exceeds the range described above, the decomposition reaction of the protein proceeds too much, and the targeted processability is not balanced with the physical properties.

In the present invention, peptidase, cellulase, pectinase, esterase and amylase in addition to the enzymes described above can be used in combination.

Also, in adding such enzymes, capable of being used are other additives, for example, phosphates such as monopotassium phosphate, dipotassium phosphate and sodium phosphate, acetates such as potassium acetate and sodium acetate, acids such as sulfuric acid, acetic acid, hydrochloric acid, citric acid and succinic acid or salts thereof, ammonia, sodium hydroxide, potassium hydroxide, sodium carbonate and sodium hydrogencarbonate.

In the present invention, the enzyme treatment described above is carried out at a temperature of 70° C. or lower, preferably 60° C. or lower and more preferably 50° C. or lower.

If the enzyme treatment temperature described above exceeds 70° C., the natural rubber latex is reduced in a stability and coagulated during the enzyme treatment. After coagulation, the decomposing effect with the enzyme is reduced. This makes it difficult to produce the natural rubber.

The natural rubber latex according to the present invention is preferably treated while using a surfactant in combination with the enzyme treatment described above. Nonionic surfactants, anionic surfactants, cationic surfactants and amphoteric surfactants can be used as the surfactant, and nonionic surfactants and anionic surfactants are particularly preferably used.

Suited as the nonionic surfactants are, for example, polyoxyalkylene ether base, polyoxyalkylene ester base, polyhydric alcohol fatty acid ester base, saccharide fatty acid ester base and alkylpolyglycoside base.

Suited as the anionic surfactants are, for example, carboxylic acid base, sulfonic acid base, sulfate base and phosphate base.

The carboxylic acid base surfactants include, for example, fatty acid salts, polyvalent carboxylic acid salts, rosin acid salts, dimer acid salts, polymer acid salts and tall oil fatty acid salts. The sulfonic acid base surfactants include, for example, alkylbenzenesulfonates, alkylsulfonates, alkylnaphthalenesulfonates, naphthalenesulfonates and diphenylethersulfonates. The sulfate base surfactants include, for example, alkylsulfate salts, polyoxyalkylenealkylsulfate salts, polyoxyalkylenealkylphenylethersulfates, tristyrenated phenol sulfate salts and polyoxyalkylenedistyrenated phenol sulfate salts. The phosphate base surfactants include alkylphosphate salts and polyoxyalkylenephosphate salts.

The natural rubber latex subjected to the enzyme treatment in the manner described above is coagulated without completely separating the non-rubber components. If separating the non-rubber components, the anti-aging property is inferior. A rubber component obtained by coagulating the treated latex described above is washed and then dried by means of a conventional dryer such as a vacuum dryer, an air dryer and a drum dryer, whereby the natural rubber according to the present invention can be obtained.

In the natural rubber latex described above, a Mooney viscosity (ML₁₊₄) and a stress relaxation time T₈₀ satisfy the relation of T₈₀<0.0035exp(ML₁₊₄/8.2)+20 in a range of 40<ML₁₊₄<100

Provided that ML₁₊₄ is a measured value at a temperature of 100° C., and T₈₀ is time (second) spent until the value of ML₁₊₄ is reduced by 80% since rotation of a rotor is stopped immediately after measurement of ML_(1+4.)

The natural rubber latex in which T₈₀ and ML₁₊₄ described above fall in the ranges described above is sufficiently small in a Mooney viscosity and a stress relaxation time, and therefore the processability is enhanced.

In the rubber composition using such natural rubber according to the present invention, at least 5 mass % of the natural rubber described above based on the whole rubber components is preferably contained therein. If this amount is less than 5 mass %, the rubber composition having the desired physical properties is not obtained in a certain case. The preferred content of this natural rubber is 10 mass % or more.

The rubber component used in combination with the natural rubber described above includes conventional natural rubbers and diene base synthetic rubbers, and the diene base synthetic rubber includes, for example, a styrene-butadiene copolymer (SBR), polybutadiene (BR), polyisoprene (IR), a butyl rubber (IIR), an ethylene-propylene copolymer and mixtures thereof.

A filler blended in the rubber component of the present invention shall not specifically be restricted, and capable of being used are compounds usually used in the rubber industry such as carbon black, silica, alumina, aluminum hydroxide, clay and calcium carbonate. Capable of being used as carbon black are, for example, carbon blacks of various grades such as SAF, HAF, ISAF, FEF and GPF. Further, silica shall not specifically be restricted, and wet silica, dry silica and colloidal silica are preferred. Such fillers can be used alone or in a mixture of two or more kinds thereof.

The total blending amount of such fillers falls in a range of preferably 30 to 120 mass parts, more preferably 40 to 80 mass parts per 100 mass parts of the rubber component.

The rubber component of the present invention can contain, if desired, various chemicals usually used in the rubber industry, for example, vulcanizing agents, vulcanization accelerator, process oils, antioxidants, scorching retarder, zinc oxide and stearic acid as long as the objects of the present invention are not damaged.

The rubber composition of the present invention can be used as well for uses in industrial products such rubber cushions, belts, hoses and others. In particular, it can suitably be used as a rubber for tires and can be applied to every tire member such as, for example, a tread rubber (including a cap rubber and a base rubber), a side wall, a ply coating rubber and a bead filler rubber.

EXAMPLES

The present invention shall be explained with reference to examples, but the constitution of the present invention shall not be restricted to the following examples.

Production Process for Natural Rubber

Production Example 1

-   (1) Enzyme treating step of natural rubber latex Levenol WX (sodium     polyoxyethylenealkylethersulfate: manufactured by Kao Corporation)     1.5 g as a surfactant was added to 1000 g of latex obtained by     adding water to natural rubber latex treated with clonal specie GT-1     and 0.4 wt % of NH₃ to control a solid content to 15 wt %, and the     latex was stirred and dispersed. Next, 0.15 g of lipase (Lipase M     “Amamo” 10: manufactured by Amano Enzyme Co., Ltd.) was added     thereto, stirred and dispersed, and then the latex was left standing     still for 15 hour. -   (2) Coagulating and drying step

Next, formic acid was added to control pH of the latex to 4.7 to thereby coagulate the latex. This solid matter was subjected five times to a craper and passed through a shredder to be turned into a crumb, followed by drying at 110° C. for 210 minutes by means of a hot air dryer, whereby a natural rubber A was obtained.

Production Examples 2 to 6

Lipase OF (manufactured by Meito Co., Ltd.) 0.15 g was added in Production Example 2 instead of adding Lipase M “Amamo” 10 described above in Production Example 1 to produce natural rubber. The natural rubber thus obtained was designated as B. In Production Example 3, Phospholipase Al (manufactured by Sankyo Co., Ltd.) 0.15 g was added instead of adding Lipase M “Amamo” 10 to produce a natural rubber. The natural rubber thus obtained was designated as C. In Production Example 4, 0.03 g of Lipase M “Amamo” 10 was added to produce a natural rubber. The natural rubber thus obtained was designated as D. In Production Example 5, a protease enzyme (“Alkarase 2.5L, type X”, manufactured by Novozymes Co., Ltd.) 0.15 g in addition to Lipase M “Amamo” 10 used in Production Example 1 was further added to produce a natural rubber. The natural rubber thus obtained was designated as E. In Production Example 6, a protease enzyme (“Proleather FG-F”, manufactured by Amano Enzyme Co., Ltd.) 0.15 g in addition to Lipase M “Amamo” 10 used in Production Example 1 was further added to produce a natural rubber. The natural rubber thus obtained was designated as F.

Comparative Production Examples 1 to 3

In Comparative Production Example 1, only the protease enzyme (“Alkarase 2.5L, type X”, manufactured by Novozymes Co., Ltd.) 0.15 g was added in place of Lipase M “Amamo” 10 used in Production Example 1 to produce a natural rubber. The natural rubber thus obtained was designated as G.

In Comparative Production Example 2, the protease enzyme (“Proleather FG-F”, manufactured by Amano Enzyme Co., Ltd.) 0.15 g was used in place of Lipase M “Amamo” 10 used in Production Example 1 to produce natural rubber. The natural rubber thus obtained was designated as H.

In Comparative Production Example 3, natural rubber latex was directly coagulated and dried without passing through the enzyme treating step of the latex to produce natural rubber. The natural rubber thus obtained was designated as I.

Production Examples 7 to 8

In Production Example 7, 0.005 g of Lipase M “Amamo” 10 used in Production Example 1 was added to produce natural rubber. The natural rubber thus obtained was designated as J. In Production Example 8, 1.00 g of Lipase M “Amamo” 10 used in Production Example 1 was added to produce natural rubber. The natural rubber thus obtained was designated as K.

Reference Production Example 1

In Reference Production Example 1, natural rubber was prepared in the same manner as in Production Example 1, except that a natural rubber latex was treated in a water bath at a temperature of 80° C. in the enzyme treatment. The natural rubber thus obtained was designated as L.

The molecular weights and the Mooney viscosity (ML₁₊₄, 100° C.) of the respective natural rubbers are shown in the following Table 1. TABLE 1 Sample Treating Molecular ML₁₊₄ T₈₀ name Enzyme name temperature (° C.) weight (Mw) (100° C.) (sec) Production Example 1 A Lipase M “Amamo” 25 1390000 71 21.4 10 (0.15 g) Production Example 2 B Lipase OF 25 1510000 73 22.7 (0.15 g) Production Example 3 C Phospholipase A1 25 1370000 72 20.3 (0.15 g) Production Example 4 D Lipase M “Amamo” 25 1340000 69 18.5 10 (0.03 g) Production Example 5 E Lipase M “Amamo” Alkarase 2.5 L 25 1250000 69 15.2 10 (0.15 g) (0.15 g) Production Example 6 F Lipase M “Amamo” Proleather 25 1280000 68 16.1 10 (0.15 g) FG-F (0.15 g) Comparative G — Alkarase 2.5 L 25 1270000 69 32.4 Production Example 1 (0.15 g) Comparative H — Proleather 25 1300000 68 31.6 Production Example 2 FG-F (0.15 g) Comparative I — 25 1620000 78 78.5 Production Example 3 Production Example 7 J Lipase M “Amamo” 25 1590000 77 70.9 10 (0.05 g) Production Example 8 K Lipase M “Amamo” 25 1130000 62 13.7 10 (1.0 g) Reference Production L Lipase M “Amamo” 80 1510000 75 62.3 Example 1 10 (0.15 g)

The respective natural rubbers described above were used to prepare rubber compositions in compositions shown in the following Table 2, and the rubber compositions thus prepared were vulcanized on the conditions of temperature of 145° C. and 33 minutes to obtain experimental rubbers. TABLE 2 Respective components of rubber compositions Mass part Natural rubber (respective examples) 100 Carbon black N339 50 Aromatic oil 5 Stearic acid 2 Antioxidant 6C (*1) 1 Zinc oxide 3 Vulcanization accelerator DZ (*2) 0.8 Sulfur 1 *1 Antioxidant 6C: N-phenyl-N-1,3-dimethylbutyl-p-phenylenediamine *2 Vulcanization accelerator DZ: N,N-dicyclohexyl-2-benzothiazolysulfenamide

The characteristics of the respective experimental rubbers were measured and evaluated by the following methods, and the results thereof are shown in Table 3.

Evaluation Methods

-   (1) Mooney viscosity of natural rubber

The Mooney viscosity (ML₁₊₄/100° C.) was measured at 100° C. according to JIS K6300-1994.

-   (2) Mooney viscosity of compound (rubber composition)

The Mooney viscosity (ML₁₊₄/130° C.) was measured at 130° C. according to JIS K6300-1994. The smaller this value is, the more excellent the processability is.

-   (3) Physical properties     -   (a) Shrinking property

A uncured rubber was wound on a 3 inch roll of roll temperature of 70° C. at a roll interval of 2 mm to rotate the roll for 2 minutes. Then, the roll was stopped rotating and left standing for one minute, and a line of 6 cm was cut thereon. After left standing for 3 minutes, a shrinking degree of the line of 6 cm was measured and shown by an index, wherein Comparative Production Example 3 was a control (100). The smaller the numerical value is, the better the shrinking property is.

-   -   (b) Tensile strength

The strength (Tb) in breaking was measured according to JIS K6301-1995.

-   -   (c) tan δ (loss factor)

A viscoelasticity-measuring apparatus (manufactured by Rheometrix Co., Ltd.) was used to measure tan δ (50° C.) at a temperature of 50° C., a distortion of 5% and a frequency of 15 Hz. The smaller the tan δ (50° C.) is, the lower the hysteresis loss property is.

-   -   (c) Abrasion resistance

A Lambourn type abrasion tester was used to measure an abrading amount at a slipping rate of 60% at room temperature and shown by an index, wherein Comparative Production Example 3 was control (100). The smaller the numerical value is, the better the abrasion resistance is. TABLE 3 Natural Contrac- Abrasion rubber ML₁₊₄ tion Tb resistance used (130° C.) index (MPa) tan δ index Example 1 A 55 72 27.1 0.191 103 Example 2 B 58 77 27.5 0.190 103 Example 3 C 56 71 27.3 0.193 101 Example 4 D 54 72 27.2 0.193 100 Example 5 E 52 69 27.6 0.197 101 Example 6 F 52 70 27.2 0.196 102 Compar- G 53 84 27.6 0.192 103 ative Example 1 Compar- H 56 87 27.4 0.193 103 ative Example 2 Compar- I 65 100 27.3 0.196 100 ative Example 3 Example 7 J 64 100 27.4 0.194 100 Example 8 K 48 65 25.2 0.201 92 Reference L 63 99 27.6 0.196 99 Example 1

In Examples 1 to 6 in the present invention, the abrasion resistance indices are excellent as compared with those in Comparative Examples 1 to 3 without reducing the breaking physical property, the low heat-generating property and the abrasion resistance.

Further, they are low as well in a compound Mooney viscosity and excellent in a processability as compared with Comparative Example 3.

INDUSTRIAL APPLICABILITY

As described above, the natural rubber latex and the natural rubber according to the present invention are shortened in a stress relaxation time and improved in a processability because phospholipid is decomposed. Further, in a rubber composition using such natural rubber, for example, a tire, the physical properties such as an aging resistant characteristic, a tensile strength and an abrasion resistance are sufficiently maintained, and the industrial applicability thereof is enhanced. 

1. A natural rubber latex in which phospholipid contained in the latex is decomposed.
 2. The natural rubber latex as described in claim 1, wherein enzyme treatment with lipase and/or phospholipase is carried out in the decomposition.
 3. The natural rubber latex as described in claim 2, wherein an addition amount of the lipase and/or the phospholipase falls in a range of 0.005 to 0.5 mass part per 100 mass parts of the latex solid component.
 4. The natural rubber latex as described in claim 2, wherein enzyme treatment with protease is carried out.
 5. The natural rubber latex as described in claim 2, wherein the enzyme treatment is carried out at a temperature of 70° C. or lower.
 6. The natural rubber latex as described in claim 2, wherein treatment with a surfactant is carried out in addition to the enzyme treatments.
 7. A natural rubber obtained from the natural rubber latex as described in claim
 1. 8. The natural rubber as described in claim 7, wherein a Mooney viscosity (ML₁₊₄) and a stress relaxation time T₈₀ of the above rubber satisfy the relation of T_(80<0.0035)exp(ML₁₊₄/8.2)+20 in a range of 40<ML₁₊₄<100 (provided that ML₁₊₄ is a measured value at a temperature of 100° C., and T₈₀ is time (second) spent until the value of ML₁₊₄ is reduced by 80% since rotation of a rotor is stopped immediately after measurement of ML₁₊₄).
 9. A rubber composition using the natural rubber as described in claim
 7. 10. A tire characterized by using the rubber composition as described in claim
 9. 11. A production process for a natural rubber, wherein it is produced by subjecting a natural rubber latex to enzyme treatment with lipase and/or phospholipase.
 12. The production process for a natural rubber as described in claim 11, wherein the enzyme treatment is carried out by adding lipase and/or phospholipase in an amount falling in a range of 0.005 to 0.5 mass part per 100 mass parts of the latex solid component.
 13. The production process for a natural rubber as described in claim 11, wherein enzyme treatment with protease is carried out in addition to the enzyme treatment described above.
 14. The production process for a natural rubber as described in claim 11, wherein the enzyme treatment is carried out at a temperature of 70° C. or lower.
 15. The production process for a natural rubber as described in claim 11, wherein treatment with a surfactant is carried out in addition to the enzyme treatment. 